JPS6025712B2 - Double effect absorption chiller/heater - Google Patents

Double effect absorption chiller/heater

Info

Publication number
JPS6025712B2
JPS6025712B2 JP11407977A JP11407977A JPS6025712B2 JP S6025712 B2 JPS6025712 B2 JP S6025712B2 JP 11407977 A JP11407977 A JP 11407977A JP 11407977 A JP11407977 A JP 11407977A JP S6025712 B2 JPS6025712 B2 JP S6025712B2
Authority
JP
Japan
Prior art keywords
refrigerant
heater
generator
liquid
temperature generator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP11407977A
Other languages
Japanese (ja)
Other versions
JPS5447150A (en
Inventor
良則 新保
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tokyo Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP11407977A priority Critical patent/JPS6025712B2/en
Publication of JPS5447150A publication Critical patent/JPS5447150A/en
Publication of JPS6025712B2 publication Critical patent/JPS6025712B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/006Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は吸収式冷凍機を利用して冷房用の冷水と暖房用
の温水を適宜機外に供V給することのできる吸収冷温水
機の改良に関し、特に、冷房から暖房への切替操作の簡
易化暖房運転時のトラブルの減少、低温熱交換器におけ
る吸収液の結晶生成の防止や融解等、多目的の冷煤濃度
調整装置を備えた二重効用吸収袷温水機を得ることを目
的とするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in an absorption chiller/heater that can appropriately supply cold water for cooling and hot water for heating to the outside of the machine by using an absorption chiller. A dual-effect absorption water heater equipped with a multi-purpose cold soot concentration adjustment device that simplifies switching operations from heating to heating, reduces trouble during heating operation, and prevents crystal formation and melting of absorption liquid in low-temperature heat exchangers. The purpose is to obtain.

以下に本発明を図面に従い説明すると、二重効用吸収冷
温水機は高温発生器1、低温発生器2、凝縮器3、蒸発
器4、吸収器5、熱交換器6,7及び溢水器8を主な構
成要素とするものであり、冷房時には弁9,9′を閉止
することにより温水器8以外の要素が、暖房時には弁1
0,−10′,10rを閉止することにより高温発生器
1と温水器8のみが作動するように構成したものである
The present invention will be described below with reference to the drawings. The double-effect absorption chiller/heater includes a high temperature generator 1, a low temperature generator 2, a condenser 3, an evaporator 4, an absorber 5, heat exchangers 6 and 7, and a water overflow device 8. The main components are: during cooling, by closing valves 9 and 9', elements other than water heater 8 are closed, and during heating, valve 1 is closed.
By closing ports 0, -10' and 10r, only the high temperature generator 1 and water heater 8 are operated.

すなわち、弁9,9′を閉止し、弁10,10′,10
″を開放した冷房時においては、高温発生器1からの高
温冷煤が冷煤管11を経て低温発生器2に流入し、該発
生器内の中間濃度の吸収液に熱を与えて一部凝縮した後
、低温冷煤管12を経て凝縮器3に流入する。一方、高
温発生器1において冷媒が加熱分離された中間濃度の吸
収液は高温熱交換器7を経て低温発生器2に流入し、上
記のように再加熱されて冷媒を更に分離し、濃吸収液と
なって濃液管13、低温熱交換器6を経て吸収器5に流
入する。一方、低温冷煤管12及び低温発生器2から凝
縮器3に流入した冷媒は、蒸発器4に散布され、蒸発器
内の冷水器14を流れる水を冷却して冷房用冷水にする
と共に、この冷水から熱を奪った冷煤は気化し吸収器5
中に散布された吸収液に吸収される。
That is, valves 9 and 9' are closed, and valves 10, 10', and 10 are closed.
'' is opened during cooling, high-temperature cold soot from the high-temperature generator 1 flows into the low-temperature generator 2 via the cold soot pipe 11, heats the intermediate concentration absorption liquid in the generator, and partially After being condensed, it flows into the condenser 3 via the low-temperature cold soot pipe 12. On the other hand, the intermediate concentration absorption liquid from which the refrigerant was separated by heating in the high-temperature generator 1 flows into the low-temperature generator 2 via the high-temperature heat exchanger 7. The refrigerant is further separated by being reheated as described above, and becomes a concentrated absorption liquid, which flows into the absorber 5 via the concentrated liquid pipe 13 and the low-temperature heat exchanger 6. On the other hand, the low-temperature cold soot pipe 12 and the low-temperature The refrigerant that has flowed into the condenser 3 from the generator 2 is sprayed into the evaporator 4, which cools the water flowing through the water cooler 14 in the evaporator and turns it into cold water for air conditioning. is vaporized and absorber 5
It is absorbed by the absorption liquid sprinkled inside.

冷煤を吸収した稀吸収液は低温熱交換器6、高温熱交換
器7を経て再び高温発生器1に流入する回路を構成する
。尚、弁9,9′を開放し、弁10,10′,10″を
閉止した暖房時においては、高温発生器1で加熱分離さ
れた高溢冷煤が温水器8内の加熱管15に凝縮潜熱を与
え、袷媒自身は液化して再び高温発生器1に流入する回
路を構成する。
The diluted absorption liquid that has absorbed cold soot passes through a low temperature heat exchanger 6 and a high temperature heat exchanger 7, and then flows back into the high temperature generator 1, forming a circuit. Note that during heating with the valves 9 and 9' open and the valves 10, 10', and 10'' closed, the overflowing cold soot heated and separated by the high temperature generator 1 flows into the heating pipe 15 in the water heater 8. A circuit is formed in which latent heat of condensation is applied, and the medium itself is liquefied and flows into the high temperature generator 1 again.

しかし、このような吸収冷温水機を実際に運転する場合
、例えば、冷房時においては低温熱交換器の濃液側で吸
収液の結晶が生じて冷凍機能を阻害したり、暖房時にお
いては吸収液によって発生器の壁面の腐蝕が急に進んだ
り、首部における液冷媒の潜溜によって発生器の液温が
異状に高なる等の弊害を伴ない易いものである。
However, when such an absorption chiller/heater is actually operated, for example, during cooling, absorption liquid crystals may form on the concentrated liquid side of the low-temperature heat exchanger, inhibiting the refrigeration function, or during heating, absorption may occur. This tends to cause problems such as rapid corrosion of the wall surface of the generator due to the liquid and an abnormally high temperature of the liquid in the generator due to latent accumulation of liquid refrigerant in the neck.

斯る点に鑑み、本発明においては、多目的の濃度調整用
冷媒タンク16を付設し、上記の諸弊害その他を除去す
ると共に、冷暖房の切替操作を簡易化するようにしたも
のであり、冷煤タンク16と冷煤ポンプ17の吐出口1
8、及び高温発生器の気相部19に蓮適する袷煤出口2
0とを、夫々開閉弁21,22を有する袷煤補給管23
,24で接続すると共に、蒸発器4、低温発生器の袷媒
管12及び低温熱交換器の濃液側25と濃度調整用冷煤
タンク16との間は、開閉弁26,27,28を有する
冷煤管29,30,31で接続したものである。
In view of this, in the present invention, a multi-purpose concentration adjustment refrigerant tank 16 is attached to eliminate the above-mentioned problems and others, and to simplify the switching operation between air conditioning and heating. Discharge port 1 of tank 16 and cold soot pump 17
8, and a soot outlet 2 suitable for the gas phase part 19 of the high temperature generator.
0 and a soot supply pipe 23 having on-off valves 21 and 22, respectively.
, 24, and on-off valves 26, 27, 28 are connected between the evaporator 4, the low-temperature generator liner pipe 12, the concentrated liquid side 25 of the low-temperature heat exchanger, and the cold soot tank 16 for concentration adjustment. They are connected by cold soot pipes 29, 30, and 31.

このような構成を有する本発明の吸収冷温水機において
は、吸収冷凍サイクル中へ充填する冷嬢量を冷煤タンク
16の内容積分だけ多く充填しておく。
In the absorption chiller/heater of the present invention having such a configuration, the amount of refrigeration to be filled into the absorption refrigeration cycle is increased by the volume of the cold soot tank 16.

而して、冷媒タンク16に冷媒を溜めるには、弁22,
27,28を閉、弁21,26を開□して冷房運転を行
えば、液冷煤はポンプ17によってタンク16に補給さ
れ、余剰分は冷煤管29、蒸発器4を経て再びポンプ1
7に吸入される。このような蒸発器4への液冷嬢の溢流
を蒸発器4に取り付けたサィトグラス32で確認した後
、弁21を閉じ次いで、弁26を閉じると濃度調整用冷
嫌タンク16には袷煤が充満され、冷凍サイクル中に余
分に充填された冷媒を分離して貯、溜できるため吸収液
の濃度は冷房運転に適した濃度となり、弁21,22,
26,27,28を閉じた状態で通常の冷房運転に移行
し、機外に冷水を供給することができる。また、液冷煤
をタンク16に補給する際、弁21の全開時間を調節す
ることによって、袷媒ポンプ17でタンク16へ送る液
冷媒の量を調節することもできる。このようにすれば、
濃度調整用冷煤タンク16には必要量だけの液冷煤を溜
めることができ、冷房負荷が冷却水温度などの外部条件
の影響を受けることなく濃度調整を適切かつ簡便に行な
うことができる。なお、このようにする場合には、タン
ク16の容量を余分に充填した冷媒の量よりも大きくす
れば良い。斯る冷房運転中、低温熱交換器の濃液側25
に吸収液の結晶が発生した場合(又は結晶の蓋然性が高
くなった場合)弁28を開き、次いで弁22開くと、冷
媒タンクの液袷煤は高温発生器の気相部19からの圧力
によって押し出され、濃吸収液に混入してその結晶を融
解したり、結晶点に近接していた吸収液の濃度を低下し
結晶のおそれを防止する。
Therefore, in order to store the refrigerant in the refrigerant tank 16, the valve 22,
27 and 28 are closed and valves 21 and 26 are opened to perform cooling operation, the liquid cooled soot is replenished into the tank 16 by the pump 17, and the surplus goes through the cold soot pipe 29 and the evaporator 4, and then is pumped back to the pump 1.
7 is inhaled. After confirming the overflow of liquid cooling to the evaporator 4 using the sight glass 32 attached to the evaporator 4, the valve 21 is closed, and then the valve 26 is closed. Since the refrigerant filled in excess in the refrigeration cycle can be separated and stored, the concentration of the absorption liquid becomes a concentration suitable for cooling operation, and the valves 21, 22,
With 26, 27, and 28 closed, normal cooling operation can be started and cold water can be supplied to the outside of the machine. Furthermore, when replenishing the tank 16 with liquid cooled soot, the amount of liquid refrigerant sent to the tank 16 by the liner pump 17 can also be adjusted by adjusting the time when the valve 21 is fully open. If you do this,
The concentration adjustment cold soot tank 16 can store a necessary amount of liquid cooled soot, and the concentration can be adjusted appropriately and easily without the cooling load being affected by external conditions such as cooling water temperature. In this case, the capacity of the tank 16 may be made larger than the amount of extra refrigerant. During such cooling operation, the concentrated liquid side 25 of the low temperature heat exchanger
When crystals of the absorption liquid occur (or when the probability of crystal formation increases), the valve 28 is opened, and then the valve 22 is opened. It is extruded and mixed into the concentrated absorption liquid to melt the crystals, or to reduce the concentration of the absorption liquid near the crystallization point to prevent the risk of crystal formation.

このような結晶融解の従来の操作は、熱交換器を外部か
ら加熱したり、液冷蝶を補給する必要がある場合には機
外から補給するために専用知識を有する技術者の煩雑な
操作を必要とするのみならず、機内には空気の編入を伴
ない易いものであったが、本発明においては単に二つの
弁の操作のみで此等のいずれの弊害も伴なうものではな
く、簡単な操作によって従来と同様な結晶融解機能を有
するものである。
Conventional operations for such crystal melting require complicated operations by technicians with specialized knowledge in order to heat the heat exchanger externally or to replenish the liquid cooling butterfly externally if necessary. However, in the present invention, simply operating two valves does not cause any of these disadvantages. It has the same crystal melting function as the conventional method with simple operation.

かつまた、吸収液の結晶を生じる程ではないものの、循
環している吸収液の濃度が外部条件の影響で上がり、高
温発生器1内の吸収液の濃度・沸騰温度〔飽和温度〕が
過度に上昇し始めた場合、弁28を開き、次いで弁22
を開くと、循環している吸収液がタンク16からの液冷
蝶で稀釈されて高温発生器1内の吸収液の濃度、沸騰温
度も降下する。それ故、過度に昇温した吸収液による高
温発生器1内壁面の腐食が防止される。なお、二重効用
吸収冷凍機における高温発生器の動作温度言い代えれば
吸収液の沸騰温度は、通常、一重効用吸収冷凍機におけ
る発生器のそれよりも数十度℃程高い〔冷煤に水、吸収
液に臭化リチウム水溶液を用いた場合〕ので、高温発生
器内壁面が一重効用吸収冷凍機の発生器内壁面よりも腐
食しやすい環境にある。このため、高温発生器内の吸収
液の濃度・飽和温度の過度の上昇を抑えて高温発生器の
動作温度〔吸収液沸騰温度〕の異常上昇を防ぐことは、
二重効用吸収冷凍機において、特に有用である。次に、
冷房運転から暖房運転に切替える場合、従来は、切替後
し‘よらくの間、高温発生器1の袷煤蒸気が低温発生器
2の冷媒管12へ流れつつこの管内で凝縮し続けるので
、この凝縞冷嬢で低温発生器2の袷媒管12が満たされ
るまで温水器8への冷煤蒸気の流入量が不足して十分な
暖房能力を発揮することができなかったが、本発明にお
いては、開閉弁10,10′,10″を閉止し、温水器
8と発生器1のみが作動するようにした後、弁27を開
き、次いで弁22を関とすると冷煤タンク内の液袷蝶は
袷媒管12に充満され、直ちに暖房運転に移行すること
が可能となり、切替後直ちに温水器8から所望の温水を
取出すことができる。
Furthermore, although it is not enough to cause crystals of the absorption liquid, the concentration of the circulating absorption liquid increases due to the influence of external conditions, and the concentration and boiling temperature (saturation temperature) of the absorption liquid in the high temperature generator 1 become excessive. If it starts to rise, open valve 28 and then open valve 22.
When opened, the circulating absorption liquid is diluted by the liquid cooling butter from the tank 16, and the concentration and boiling temperature of the absorption liquid in the high temperature generator 1 are also lowered. Therefore, corrosion of the inner wall surface of the high temperature generator 1 due to the excessively heated absorption liquid is prevented. The operating temperature of the high-temperature generator in a dual-effect absorption refrigerator, in other words, the boiling temperature of the absorption liquid, is usually several tens of degrees higher than that of the generator in a single-effect absorption refrigerator. , when a lithium bromide aqueous solution is used as the absorption liquid], the inner wall surface of the high-temperature generator is in an environment where it is more likely to corrode than the inner wall surface of the generator of a single-effect absorption refrigerator. Therefore, it is necessary to suppress the excessive rise in the concentration and saturation temperature of the absorption liquid in the high-temperature generator and prevent the abnormal rise in the operating temperature of the high-temperature generator (absorption liquid boiling temperature).
It is particularly useful in dual effect absorption refrigerators. next,
Conventionally, when switching from cooling operation to heating operation, the soot vapor in the high temperature generator 1 flows into the refrigerant pipe 12 of the low temperature generator 2 and continues to condense in this pipe for a while after switching. However, in the present invention, the amount of cold soot vapor flowing into the water heater 8 was insufficient until the medium pipe 12 of the low-temperature generator 2 was filled with condensation cooling, and sufficient heating capacity could not be achieved. After closing the on-off valves 10, 10', and 10'' so that only the water heater 8 and generator 1 operate, the valve 27 is opened, and then, when the valve 22 is closed, the liquid in the cold soot tank is opened. The butterflies fill the medium pipe 12, and it becomes possible to immediately shift to heating operation, and the desired hot water can be taken out from the water heater 8 immediately after switching.

尚、冷蝶が充満されたことを低温発生器のサィトグラス
で確認した後は、弁22,27を閉止するのが望ましい
It is desirable to close the valves 22 and 27 after confirming through the sight glass of the low temperature generator that the cold butterfly is filled.

これは暖房運転時において気化した冷煤が運転休止中の
機器、管路の凹所に稀溜して高温発生器1における液面
が低下したり、吸収液濃度が上って発生器内温度が異常
に高くならないようにするためである。また、本発明に
よる濃度調整用冷媒タンク16を二重効用吸収冷凍機を
構成する機器のいずれよりも高い位置に取り付けるよう
にしているので、隅々発生器の液面が異常に下ったとき
や、吸収液濃度が上りすぎるときに、弁27,22を開
いて液冷煤を供V給することにより、簡易に濃度の調整
や吸収液の沸騰温度の異常上昇による発生器内壁面の腐
蝕も防止できるものである。このように本発明の濃度調
整用冷媒タンクは、二重効用吸収袷温水機の運転時にお
いて常時必要とされる吸収液濃度の制御、吸収液結晶の
防止、高温発生器内壁面の腐蝕防止、冷房から暖房への
切替後所望の暖房能力を発揮するまでの時間の短縮など
いずれについても、その目的を達成することができるも
のであり、冷房切替式の二重効用吸収冷温水機の使用効
果を高める上で極めて有意義なものである。
This is because cold soot that vaporizes during heating operation accumulates in the recesses of equipment and pipes that are not in operation, causing the liquid level in the high-temperature generator 1 to drop, or the absorption liquid concentration to rise, causing the temperature inside the generator to rise. This is to prevent the value from becoming abnormally high. In addition, since the concentration adjusting refrigerant tank 16 according to the present invention is installed at a higher position than any of the devices constituting the double-effect absorption refrigerator, when the liquid level in the generator drops abnormally, When the absorption liquid concentration rises too much, by opening the valves 27 and 22 and supplying liquid cooled soot, it is possible to easily adjust the concentration and prevent corrosion of the generator inner wall surface due to an abnormal rise in the boiling temperature of the absorption liquid. It is preventable. As described above, the concentration adjustment refrigerant tank of the present invention can control the absorption liquid concentration, which is always required during the operation of a dual-effect absorption water heater, prevent absorption liquid crystals, prevent corrosion of the inner wall surface of the high temperature generator, It is possible to achieve both objectives, such as shortening the time it takes to achieve the desired heating capacity after switching from cooling to heating. This is extremely meaningful in increasing the quality of life.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明装置を有する二重効用吸収冷温水機の一実施
例を示す回路構成図である。 1・・・・・・高温発生器、2・・・・・・低温発生器
、3・・・・・・凝縮器、4・・・・・・蒸発器、5・
・・・・・吸収器、6・・・・・・低温熱交換器、8・
・・・・・温水器、16・…・・濃度調整用冷煤タンク
、17……冷煤ポンプ、21,22,26,27,28
・・・・・・開閉弁、23,24・・・・・・冷煤補給
管、29,30,31・・・・・・冷煤管。
The figure is a circuit configuration diagram showing an embodiment of a dual-effect absorption chiller/heater having a device of the present invention. 1... High temperature generator, 2... Low temperature generator, 3... Condenser, 4... Evaporator, 5...
...Absorber, 6...Low temperature heat exchanger, 8.
... Water heater, 16 ... Cold soot tank for concentration adjustment, 17 ... Cold soot pump, 21, 22, 26, 27, 28
......Opening/closing valve, 23,24...Cold soot supply pipe, 29,30,31...Cold soot pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 高温発生器、低温発生器、凝縮器、蒸発器、吸収器
、高温熱交換器及び低温熱交換器を配管接続し、かつ、
温水器を付設することにより冷水と温水とを適宜機外に
供給できるようにした吸収冷温水機にその構成機器のい
ずれよりも上方へ位置させて濃度調整用冷媒タンクを付
設し、該冷媒タンクと冷媒ポンプ出口及び高温発生器の
冷媒出口とを、夫々、開閉弁を有する冷媒補給管で接続
すると共に、蒸発器、低温発生器の冷媒管及び低温熱交
換器の濃液側と前記冷媒タンクとの間を開閉弁を有する
冷媒管で接続することにより、冷房時には冷媒ポンプの
圧力で冷媒タンクに冷媒を貯留して吸収液の濃度を上げ
、低温熱交換器で結晶のおそれがあるときには該熱交換
器に直接に冷媒を流入させて結晶を融解し、冷房から暖
房への切替時には冷媒タンクの液冷媒を低温発生器の冷
媒管に充満させ、かつ、高温発生器の吸収液の濃度の過
度の上昇を防止して吸収液の沸騰温度が高くなり過ぎる
のを防ぐようにしてなる二重効用吸収冷温水機。
1. Connect the high temperature generator, low temperature generator, condenser, evaporator, absorber, high temperature heat exchanger, and low temperature heat exchanger with piping, and
An absorption chiller/heater is equipped with a water heater so that cold water and hot water can be appropriately supplied outside the machine, and a refrigerant tank for concentration adjustment is attached to the absorption chiller/heater, which is located above any of its component equipment. and the refrigerant pump outlet and the refrigerant outlet of the high-temperature generator, respectively, are connected by refrigerant supply pipes each having an on-off valve, and the evaporator, the refrigerant pipe of the low-temperature generator, and the concentrated liquid side of the low-temperature heat exchanger are connected to the refrigerant tank. By connecting a refrigerant pipe with an on-off valve between the The crystals are melted by flowing the refrigerant directly into the heat exchanger, and when switching from cooling to heating, the liquid refrigerant in the refrigerant tank is filled into the refrigerant pipe of the low temperature generator, and the concentration of the absorption liquid in the high temperature generator is reduced. A dual-effect absorption chiller/heater that prevents the boiling temperature of the absorption liquid from becoming too high by preventing excessive rise.
JP11407977A 1977-09-20 1977-09-20 Double effect absorption chiller/heater Expired JPS6025712B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11407977A JPS6025712B2 (en) 1977-09-20 1977-09-20 Double effect absorption chiller/heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11407977A JPS6025712B2 (en) 1977-09-20 1977-09-20 Double effect absorption chiller/heater

Publications (2)

Publication Number Publication Date
JPS5447150A JPS5447150A (en) 1979-04-13
JPS6025712B2 true JPS6025712B2 (en) 1985-06-19

Family

ID=14628522

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11407977A Expired JPS6025712B2 (en) 1977-09-20 1977-09-20 Double effect absorption chiller/heater

Country Status (1)

Country Link
JP (1) JPS6025712B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6405558B1 (en) * 2000-12-15 2002-06-18 Carrier Corporation Refrigerant storage apparatus for absorption heating and cooling system
US6370893B1 (en) * 2000-12-22 2002-04-16 Carrier Corporation Absorption cooling system with refrigerant management for dilution and part load operation

Also Published As

Publication number Publication date
JPS5447150A (en) 1979-04-13

Similar Documents

Publication Publication Date Title
JP2000018762A (en) Absorption refrigerating machine
JPS6025712B2 (en) Double effect absorption chiller/heater
JP2003343940A (en) Absorption water cooler/heater
JP2000274864A (en) Method for controlling absorption refrigerator
JP3363518B2 (en) Operation control method of single double effect absorption refrigerator
JP2538424B2 (en) Single-double-effect absorption refrigerator
JPS5818139Y2 (en) Double effect absorption chiller
JP3086594B2 (en) Single double effect absorption refrigerator
JP2538423B2 (en) Single-double-effect absorption refrigerator
JPH07324839A (en) Single and double effect absorption hot and chilled water generator
JPS602543Y2 (en) absorption refrigerator
JP4115020B2 (en) Control method of absorption refrigerator
JPS6018764Y2 (en) Absorption chiller control device
JP3345610B2 (en) Cycle control method for absorption chiller / chiller / heater
JP2858921B2 (en) Control device for absorption refrigerator
JP2654129B2 (en) Absorption refrigerator
JPH06300382A (en) Double effect absorption type refrigerating machine
JPH11230631A (en) Absorption refrigerator
JPS6311570Y2 (en)
JPS5986876A (en) Controller for double effect absorption refrigerator
JPH10227539A (en) Absorption type refrigerating device
JPS6114429B2 (en)
JPS6113144B2 (en)
JPH03156260A (en) Absorption cold/hot water producer
JP2002323269A (en) Absorption refrigerating machine